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Thermal Effects Thermal Effects Ming Yan1,2,*, Panyue Zhang1,2, Guangming Zeng1,2 ABSTRACT: This review focuses on the research Biological Nitrogen and Phosphorus Removal literatures published in 2015 relating to topics of thermal The short-term effect of temperature on the effects in water pollution control. This review is divided maximum biomass specific activity of anaerobic into the following sections: biological nitrogen and ammonium oxidizing (anammox) bacteria was reported by phosphorus removal, wastewater treatment for organic Lotti et al. (2015). The results indicated that for the conversion, industrial wastewater treatment, anaerobic anammox conversion, the temperature dependency could digestion of sewage sludge and solid waste, sludge biochar not be accurately modeled by one single Arrhenius preparation and application, pyrolysis of sewage sludge, coefficient as typically applied for other biological reduction heavy metal in sewage sludge and soil, and other processes. The temperature effect increased at lower issues of wastewater and sludge treatment. temperatures. Adapted anammox sludge had a higher specific rate at lower temperature. Anammox sludge KEYWORDS: thermal effects, biological nitrogen and cultivated in an aerated partial nitritation/anammox process phosphorus removal, wastewater treatment for organic and/or in biofilm seemed to be less influenced be a conversion, industrial wastewater treatment, anaerobic decrease in temperature than anammox sludge grown under digestion of sewage sludge and solid waste, sludge biochar non-arated conditions and/or in suspension. preparation and application, pyrolysis of sewage sludge, Lackner et al. (2015) compared partial nitritation- reduction heavy metal in sewage sludge and soil. anammox in two laboratory-scale reactors, a sequencing batch reactor (SBR) and a moving bed biofilm reactor doi: 10.2175/106143016X14696400495730 (MBBR). Experiments were carried out with realistic ————————— seasonal temperature variations over a 1-year period. The 1*College of Environmental Science and Engineering, Hunan results revealed that both systems had to face the decrease University, Changsha 410082, PR China; Tel. +86 13607488663; of ammonium conversion rates and nitrite accumulation at Fax. +86 731 88823701; e-mail: [email protected] a temperature lower than 12 °C. The SBR did not recover 2Key Laboratory of Environmental Biology and Pollution from the loss in anammox activity even when the Control (Hunan University), Ministry of Education, Changsha temperature increased again. The MBBR only showed a 410082, PR China 1808 Water Environment Research, Volume 88, Number 10—Copyright © 2016 Water Environment Federation short nitrite peak and recovered its initial ammonium (2015). The reactors were operated at a total nitrogen (TN) turnover when the temperature rose back to >15 °C. concentrations in the range of 5-20 mg/L. Anammox The influence of temperature on the anammox activities reached 465 mg/L∙d at 29 °C with minimum process for high salinity wastewater was investigated by doubling time of 18 d. The Lower temperature of 12.5 °C Xing et al. (2015). Four upflow anaerobic sludge blanket resulted in a significant decrease in activity to 46 mg/L∙d reactors were operated in parallel at ambient temperatures and the doubling time was 79 d. from 25 to 9 °C and thermostatic room temperatures of 35 A novel system integrating Johannesburg (JHB) ± 2 °C. The results demonstrated that low ambient and sulfur autotrophic denitrification (SAD) process was temperature and high sodium levels impaired the nitrogen proposed by Li et al. (2015), to enhance nitrogen removal removal performance of anammox granular sludge. The in treating low COD/TN ratio (COD 129 mg/L, TN 29 anaerobic ammonium-oxidizing bacteria gradually adapted mg/L on average) municipal wastewater at low temperature to a salt concentration of 15 g/L at low ambient temperature, (12.2 ± 0.5 °C). The results showed that under a HRT of 3 + and a nitrogen removal rate of 1.34 ± 0.12 kg N/m ∙d was 11.3 h, the average effluent COD, TN, and NH4 -N of JHB achieved, compared with 1.90 ± 0.01 kg N/m3∙d at a salt process were 32, 13.8, and 1.6 mg/L, respectively. It was concentration of 15 g/L and a temperature of 35 ± 2 °C. found that 87.0 % JHB effluent nitrogen was removed by Partial nitritation for a low-strength wastewater SAD process under the most efficient nominal hydraulic + (70 mg NH4 –N) at low temperature was stably achieved in retention time (HRT) of 0.32 h. The SAD process effluent + an aerobic granular reactor in continuous mode (Isanta et of COD, TN, and NH4 –N were 21, 1.8, and 1.0 mg/L, al., 2015). The temperature progressively decreased from respectively. Most importantly, the JHB-SAD system could 30 to 12.5 °C, and a suitable effluent nitrite to ammonium achieve complete nitrogen removal theoretically as long as + concentrations ratio to a subsequent anammox reactor was the NH4 –N was sufficiently oxidized. maintained stable during 300 days at 12.5 °C. The average With inoculum sludge from a conventional applied nitrogen loading rate at 12.5 °C was 0.7 ± 0.3 g activated sludge wastewater treatment plant, the formation N/L∙d, with an effluent nitrate concentration of only 2.5 ± of aerobic granular sludge (AGS) for simultaneous organic - 0.7 mg NO3 –N/L. The biomass fraction of nitrite-oxidizing and nutrient removal in three SBRs at different high bacteria in the granular sludge decreased from 19% to only temperatures (30, 40 and 50 ± 1 °C) was studied by Halim 1% in 6 months of reactor operation at 12.5 °C. Nitrobacter et al. (2015). The complete cycle time of SBRs was 3 h. spp. were found as the dominant NOB population, whereas The results revealed that granules developed at 50 °C have Nitrospira spp. were not detected. the highest average diameter of 3.36 mm, and the removal Activity and growth of anammox biomass on efficiency of COD, ammonia and phosphate was 98.17%, municipal wastewater was researched by Michele et al. 94.45% and 72.46%, respectively. The study also 1809 Water Environment Research, Volume 88, Number 10—Copyright © 2016 Water Environment Federation demonstrated that the AGS formed at high temperatures and the AAO showed a better performance at SRT of 5–25 was suitable for hot climate conditions. d under the same operating cost for its higher pollutant Liu et al. (2015) studied the accumulation of removal efficiency and concentration of phosphorus- denitrifying polyphosphate-accumulating organisms accumulating organisms. Furthermore, the optimal (DNPAOs) using an improved SBR system in which condition was obtained using mixed liquor recirculation of anaerobic-aerobic-anoxic and anaerobic-anoxic were 100%, returned activated sludge of 50%, and SRT of 16 d. adopted at a low temperature of 15 °C. The results Sayi-Ucar et al. (2015) conducted a long-term indicated that it was feasible to accumulate DNPAOs with study on the impact of high temperature on enhanced concurrent nitrogen and phosphorus removals in the biological phosphorus and nitrogen removal in membrane improved SBR system. Moreover, a DNPAOs strain was bioreactor. The MBR system was operated at relatively isolated and was identified as Acinetobacter sp. J6. The high temperatures (24–41 °C). The TP removal gradually strain J6 had the highest N and P removal rates under an increased from 50% up to 95% while the temperature original pH of 8.0, a total phosphorus (TP) concentration of descended from 41 to 24 °C. At high temperatures, 4.16 mg/L and a temperature of 15 °C. anaerobic volatile fatty acid (VFA) uptake occurred with Dong et al. (2015) produced immobilized pellets low phosphorus release implying the competition of entrapping activated sludge in waterborne polyurethane, glycogen accumulating organisms (GAOs) with + and applied to treat ammonium (NH4 –N) synthetic polyphosphate accumulating organisms (PAOs). The gross wastewater in SBRs at low temperatures. The oxygen membrane flux was 43 LMH corresponding to the specific uptake rate of immobilized pellets reached 240.83±15.59 permeability of 413 LMH/bar at 39 °C in the MBR tank. mg O2/(L∙h), and the oxygen was primarily consumed by The specific permeability increased by the factor of 43% at the bacteria on the pellet surfaces (0–600 μm). The dosing 39 °C compared to that of 25 °C during long-term of the pellets (30 ml/L) into an SBR significantly improved operation. the nitrification efficiency at low temperatures of 7–11 °C, Ma et al. (2015) assessed a long-term + achieving an average NH4 –N removal of 84.09%, which is investigation of a novel electrochemical membrane higher than the removal of 67.46% observed for the control bioreactor (EMBR) for low-strength municipal wastewater group. treatment under low temperature. At lower temperatures Modeling of multimode anaerobic/anoxic/aerobic (<10–15 °C), power production in the EMBR was (AAO) wastewater treatment process at low temperature of negligible and therefore the integration did not improve the 12.5 °C was studied by Zhou et al. (2015). Influences of reactor performance. With the rebound of water sludge retention time (SRT) on effluent quality, functional temperature over 15–20 °C, efficient redox reactions were biomass and operating cost were evaluated for each mode, achieved in the EMBR, which subsequently resulted in 1810 Water Environment Research, Volume 88, Number 10—Copyright © 2016 Water Environment Federation sludge reduction (27.3% lower than the control MBR) and removal by Scenedesmus sp. were obtained as model membrane fouling alleviation. The total nitrogen removal parameters. efficiency of the EMBR averaged 78.2% at high Cho et al. (2015) evaluated the factors temperatures, despite the decrease of organic loading rate influencing diversity and growth of indigenous algal of the feed for heterotrophic denitrification. Energy balance consortium cultivated on untreated municipal wastewater in analysis indicated that the total energy consumption of the a high rate algal pond (HRAP) for a period of 1 year.
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